Isobaric vapor-liquid equilibria for the binary systems isobutyl alcohol + isobutyl acetate and tert-butyl alcohol + tert-butyl acetate at 20 and 101.3 kPa Montón, J.; Muñoz, R.; Burguet, M.; Torre, J.d.l.; Fluid Phase Equilibria 2005, 227, 19-25
- Journal: Fluid Phase Equilibria
- Sample Quantity(ies): Vapor pressure
- Methodology: EBULLIO:UFactor:8
- Phase(s): Liquid
- Substances:
Data
| T (K) | P (kPa) |
| 307.53 | 8.99 |
| 339.58 | 35.02 |
| 342.46 | 39.04 |
| 345.75 | 43.98 |
| 348.84 | 49.09 |
| 352.07 | 54.94 |
| 354.95 | 60.02 |
| 357.17 | 65.33 |
| 359.63 | 70.88 |
| 361.83 | 76.15 |
| 363.85 | 81.26 |
| 311.79 | 10.99 |
| 366.00 | 87.01 |
| 367.99 | 92.58 |
| 369.46 | 96.91 |
| 370.68 | 100.64 |
| 370.86 | 100.0 |
| 372.26 | 105.59 |
| 315.64 | 13.09 |
| 319.82 | 15.73 |
| 324.28 | 19.04 |
| 325.46 | 20.0 |
| 328.94 | 23.09 |
| 332.36 | 26.48 |
| 336.12 | 30.67 |
5021; tert-butyl ethanoate; 01345